Reactant liquid system for facilitating the production of carbon nanostructures

ABSTRACT

A method includes isolating carbon atoms as conditioned carbide anions below a surface of a reactant liquid. The conditioned carbide anions are then enabled to escape from the reactant liquid to a collection area where carbon nanostructures may form. A carbon structure produced in this fashion includes at least one layer made up of hexagonally arranged carbon atoms. Each carbon atom has three covalent bonds to adjoining carbon atoms and one unbound pi electron.

CROSS-REFERENCE TO RELATED APPLICATIONS

This application is a continuation-in-part of U.S. patent applicationSer. No. 10/887,695, entitled “Method and Apparatus for Producing CarbonNanostructures,” and a continuation-in-part of U.S. patent applicationSer. No. 11/025,717, entitled “Method and Apparatus for Preparing ACollection Surface for Use in Producing Carbon Nanostructures.” TheApplicant claims the benefit of each of these applications under 35U.S.C. § 120. The entire content of each of these applications isincorporated herein by this reference.

TECHNICAL FIELD OF THE INVENTION

The present invention relates to methods for manufacturing carbonnanotubes and other carbon nanostructures from a carbon-bearingfeedstock. In particular, the invention relates to methods for placingcarbon atoms in condition to form impurity-free carbon nanostructures.The invention also includes a particular type of carbon nanostructure.

BACKGROUND OF THE INVENTION

Carbon nanostructures have received a great deal of interest since theirdiscovery. It has been suggested that carbon nanostructures may haveimportant applications in electronics, in materials sciences, and in anumber of additional fields. As used in this disclosure, a carbonnanostructure comprises a structure formed from chemically bonded carbonatoms, with or without impurities or intentionally added materialsincorporated in the carbon structure or adjacent to the carbonstructure. Carbon nanostructures include structures in which carbonatoms are arranged in generally a series of interconnected hexagonalrings formed into a tube or other structure. Carbon nanostructures maybe single walled or multiple walled nanotubes, nanofibers, nanorope, ornanowire. Single wall nanotubes include a single layer of thehexagonally arranged carbon atoms, while multiple walled nanotubes aremade up of an inner layer of carbon atoms and a series of one or moreouter layers of hexagonally arranged carbon atom structures.

Despite the interest in carbon nanostructures and the potentiallyimportant uses for such structures, the practical application of carbonnanostructures in products has been slowed by the difficulty inmanufacturing such structures. Two general types of processes have beenemployed to produce or isolate carbon nanostructures. One process typeuses a plasma arc between carbon electrodes. U.S. Pat. Nos. 5,482,601and 5,753,088 describe such carbon plasma arc processes for producingcarbon nanotubes. Another process type involves simply isolatingnaturally formed carbon nanotubes from graphite and soot. Such anisolation process or refinement process for carbon nanotubes isdescribed in U.S. Pat. No. 5,560,898.

The prior processes for producing or isolating carbon nanotubes havebeen found to produce only small quantities of carbon nanotubes ofinconsistent quality. The low quality carbon nanotubes produced orisolated by the prior methods commonly included metal or other atomsincorporated in the carbon structure. These impurities incorporated inthe walls of the carbon nanotubes may have a negative impact on thequalities and properties of the nanotube and may render it unsuitablefor an intended purpose. In particular, prior carbon nanostructureproduction techniques include no mechanism for preventing hydrogen atomsand other atoms that may be present in the carbon-bearing feed materialfrom being incorporated into the nanocarbon structure. Also, priorcarbon nanostructure production techniques tend to allow carbon from thefeed material to become incorporated into the carbon nanostructures inan unpredictable fashion outside of the desired interconnected hexagonalring structure. This inclusion of amorphous carbon in the resultingcarbon nanostructure greatly degrades the properties and usefulness ofthe resulting carbon nanostructure.

SUMMARY OF THE INVENTION

The present invention provides methods for placing carbon in conditionto form high-quality, substantially impurity-free carbon nanostructures.The present invention also encompasses a novel type of carbonnanostructure.

A method according to the present invention includes isolating carbonatoms as conditioned carbide anions below a surface of a reactantliquid. The conditioned carbide anions are then allowed to escape fromthe reactant liquid to a collection area where carbon nanostructures mayform. The isolation of carbon atoms as conditioned carbide anionsincludes two components. A first component involves separating thecarbon atoms from a carbon-bearing feed material that has beenintroduced into the reactant liquid and preventing the carbon atoms fromcombining with other materials. The second component of isolating carbonatoms as the desired conditioned carbide anions involves increasing theenergy state of the separated and isolated carbon atoms. The desiredenergy state of carbide anions within the scope of the present claims isat least the SP3 hybrid energy state, in which the carbide anions haveabsorbed greater than 22 eV (electron volt) of energy from the reactantliquid bath. Thus, a “conditioned carbide anion” within the scope of thepresent claims refers to a carbide anion at least at the SP3 hybridenergy state.

The isolation of carbon atoms as conditioned carbide anions within thescope of the present invention may be accomplished by chemicalreduction, chemical oxidation, reactions from acids, bases, or salts, orpyrolysis in the reactant liquid. For example, one preferred form of theinvention utilizes a liquid reactant metal to chemically reduce acarbon-bearing feed material to isolate carbon atoms from the feedmaterial and elevate the energy state of the isolated carbon atoms toform the desired conditioned carbon anions, that is, carbon anions atleast at the SP3 hybrid energy state. Regardless of the particularmechanism by which the reactant liquid isolates the carbon atoms,maintaining carbon atoms that have been separated from the feed materialbelow the surface of the reactant liquid allows the carbon atoms toremain isolated from each other and other materials with which bondscould form and allows the carbon atoms to be energized to the desiredconditioned state.

A carbon structure according to the present invention includes at leastone layer made up of hexagonally arranged carbon atoms. Each carbon atomhas three covalent bonds to adjoining carbon atoms and one unbound pielectron. Thus, the carbon structure according to the present inventionis a pure carbon structure, free of contaminating amorphous carbon andany other contaminating atoms. The carbon structure according to theinvention is also free of hydrogen that would otherwise form a fourthcovalent bond with each carbon atom. This contamination-free andhydrogen-free carbon structure may take the form of flat sheets ofmaterial or single or multi-walled tubes.

These and other advantages and features of the invention will beapparent from the following description of the preferred embodiments,considered along with the accompanying drawings.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 is a diagrammatic representation of an apparatus embodying theprinciples of the invention.

FIG. 2 is a diagrammatic end view of an outlet end of the reactionchamber shown in FIG. 1.

FIG. 3 is a diagrammatic representation of an alternate collectionchamber according to the present invention.

FIG. 4 is a diagrammatic representation of another alternate collectionsurface arrangement within the scope of the present invention.

FIG. 5 is a diagrammatic representation of another alternate collectionchamber according to the present invention.

FIG. 6 is a diagrammatic representation of a test apparatus that hasbeen used to produce carbon nanostructures according to the presentinvention.

FIG. 7 is a diagrammatic isometric representation of a single-walledcarbon nanostructure according to the present invention.

FIG. 8 is a diagrammatic isometric representation of a double-walledcarbon nanostructure according to the present invention.

DESCRIPTION OF PREFERRED EMBODIMENTS

The claims at the end of this application set out novel features whichthe Applicant believes are characteristic of the invention. The variousadvantages and features of the invention together with preferred modesof use of the invention will best be understood by reference to thefollowing description of illustrative embodiments read in conjunctionwith the drawings introduced above.

Referring to the diagrammatic representation of FIG. 1, an apparatus 100for producing carbon nanostructures according to the present inventionincludes a reactant liquid vessel 101 for containing a reactant liquid105 at a reactant liquid level 102. An injection arrangement showngenerally at reference numeral 103 allows a stream of feed material tobe injected into reactant liquid vessel 101 at an injection point 104below reactant liquid level 102. Apparatus 100 further includes acollection arrangement shown generally in dashed box 106. Theillustrated collection arrangement includes a collection chamber 107positioned to receive effluent escaping from the reactant liquid in aneffluent ejection area shown generally at reference numeral 108. Thecollection arrangement also includes a collection surface 110 withincollection chamber 107, the collection surface residing at a positionabove the reactant liquid level and adjacent to effluent ejection area108.

The apparatus shown in FIG. 1 includes a reaction chamber portion formedwithin vessel 101 below the reactant metal level 102. This reactionchamber is shown generally at reference numeral 112 and is defined by atunnel structure having an upper wall 114 located below the reactantliquid level 102 in vessel 101. The tunnel structure is best shown inthe end view of FIG. 2 and includes side walls 115 in addition to theupper wall 114. Referring again to FIG. 1, the tunnel structure producesan elongated tunnel below the reactant liquid level 102 in vessel 101.Feed material is injected at a feed end 116 of the tunnel structure andreaction products from the reaction of the feed material in the reactantliquid exits the tunnel structure at an outlet end 117. The figures showthese reaction products in the reactant metal as bubbles 118. Preferredforms of the tunnel structure include one or more flow channels or lips119 at the outlet end 117 that each defines a location in which therelatively light reaction products collected at the top of the tunnelstructure exit the tunnel. The importance of directing the reactionproducts to particular locations will be described further below inconnection with the collection chamber 107.

The function of the tunnel structure defined by side walls 115 and upperwall 114 is to help ensure good contact between the reactant liquid andthe feed material and between the reactant liquid and any intermediatereaction products that form from initial reactions of feed material, andto ensure sufficient residence time for the feed material and reactionproducts in the reactant liquid. This contact and residence time helpsensure the isolation of substantially all carbon from the carbon-bearingfeed material and elevation of the resulting carbon anions to thedesired conditioned carbon anions. The placement of the tunnel below thereactant liquid level 102 also ensures that a pressure is maintained onthe feed material and intermediate reaction products. This pressureresults from the column of reactant liquid above the feed material andintermediate reaction products. The tunnel structure shown in thepresent drawings includes one or more vents or passages 120 along thelength of the tunnel structure to allow fresh reactant liquid tocontinually flow into the tunnel structure along its length and to helpaccommodate the expansion of gasses in the tunnel.

The form of the invention shown in FIG. 1 includes an enclosure 121 overreactant liquid vessel 101. It will be appreciated that apparatus 100will also commonly require an arrangement for heating the reactantliquid to maintain it in a desired temperature range, and an arrangementfor circulating the reactant liquid in vessel 101 and especially throughthe reaction chamber 112 defined by the tunnel structure walls 114 and115 in the direction shown by arrow F in FIG. 1. Heating the reactantliquid may be accomplished by burning suitable hydrocarbon fuels, byelectrical induction, or by any other suitable process. Further detailson the tunnel structure and the structure of vessel 101 and arrangementsfor heating and circulating reactant liquid, particularly a liquidreactant metal such as aluminum alone or together with other metals, maybe found in U.S. Pat. No. 6,227,126, which is incorporated herein bythis reference. However, since these details are not necessary for anunderstanding of the present invention, such details are omitted here.

Feed material injection arrangement 103 includes an injection conduit124 having an outlet end that extends to injection point 104 below thereactant liquid level 102. The injection point 104 is located so thatthe feed material exiting the conduit is captured within the tunnelstructure under upper wall 114, and thus is forced to flow along theupper wall and along the entire length of the tunnel structure before itcan exit the reactant liquid in effluent ejection area 108. This flowalong the lower surface of upper tunnel wall 114 helps ensure completedestruction of the feed material and any intermediate reaction productsthat may form as the feed material is destroyed by reaction with or inthe reactant liquid, and results in the formation of the desiredisolated carbon anions in the reactant liquid. Injection point 104 isalso preferably at a depth below the reactant liquid level 102 toproduce a desired reaction pressure due to the column of reactant liquidabove the injection point. For a predominantly aluminum reactant liquid,this pressure is approximately 2.4 pounds per square inch aboveatmospheric pressure. Due to the relatively high temperature that may bepresent in the reactant liquid, conduit 124 is preferably enclosed in asuitable thermal insulating sheath 127 which may comprise one or morelayers of insulating material or a jacket through which a cooling fluidmay be circulated. The upper end of conduit 124 is connected to a linewhich ultimately extends to a feed material supply 128 and preferably apurge gas supply 129 through a suitable arrangement of control valves130.

Collection chamber 107 is located with respect to the outlet end 117 ofthe tunnel structure so that reaction products 118 are ultimatelycaptured in the collection chamber. That is, the reaction products 118flow up from flow channels 119 and traverse the surface of the reactantliquid in effluent ejection area 108 into the area defined as collectionchamber 107. This area is defined by chamber walls 134. An outletconduit 135 receives material that is not collected within chamber 107,and removes that material from the system. This material removed throughconduit 135 may include gasses such as hydrogen and nitrogen, carbon,and particulates that escape the reactant liquid bath. Although it isnot shown in FIG. 1, it will be appreciated that suitable equipment maybe connected to outlet conduit 135 to remove recoverable material fromthe effluent that reaches the outlet conduit.

In the form of the invention shown in FIG. 1, collection surface 110comprises an upper surface of a collection structure 138 that eitherfloats or is fixed so that a lower surface 139 of the structure residesbelow reactant liquid level 102 while the collection surface 110 residesabove the reactant liquid level in collection chamber 107. A deflectionsurface 140 may also be included in collection chamber 107 positioned todeflect effluent traversing the surface of the reactant liquid ineffluent ejection area 108 so that the effluent, including theconditioned carbon atoms, flow over collection surface 110. It will benoted that in the embodiment shown in FIG. 1, both collection surface110 and deflection surface 140 extend in a respective plane transverseto a device vertical axis V. Also, in the embodiment shown in FIG. 1,lower surface 139 of collection structure 138 forms a blocking structurepositioned above the respective flow channel 119 and below the reactantliquid level 102 in reactant liquid vessel 101. The effluent from thefeed material/reactant liquid reaction must flow around this blockingstructure in order to reach effluent ejection area 108 and exit thereactant liquid.

Collection surface 110 may be located from just above reactant liquidlevel 102 (an inch or less) to as much as three feet above the reactantliquid. One or more seed objects may be included on collection surface110. Seed objects may be any type of objects that encourage orfacilitate the assembly of carbon nanostructures from the conditionedcarbon atoms exiting the reactant liquid bath. Seed objects may includepure catalyst metals such as titanium and platinum, for example, ormetal oxides such as manganese oxide, magnesium oxide, copper oxide,chromium oxide, and titanium oxide, for example. The catalyst may or maynot be sacrificial. Seed objects may also include graphite surfaces,carbon surfaces, and seed carbon nanostructures. The seed objects may bespaced apart across collection surface 110 or may make up the entirecollection surface. For example, the entire collection structure 138 maybe formed from graphite or carbon or some other material that serves asa seed material. In another example, seed objects comprising atoms ofcatalyst metals may be liberated from reactant liquid 105 and depositedacross collection surface 110 as described in related U.S. patentapplication Ser. No. 11/025,717.

Referring to FIG. 3, an alternate collection surface arrangementincludes a collection structure 301 mounted on a rod 302 or othersuitable support in collection chamber 303 defined by chamber walls 306.Lower surface 304 of structure 301 provides a blocking surface similarto surface 139 shown in FIG. 1, while surface 305 provides thecollection surface in the embodiment shown in FIG. 3. This alternateembodiment is advantageous because the entire collection structure 301may be readily withdrawn from collection chamber 303 through a suitableaccess opening (not shown) in the chamber in order to gain access to thecollection surface 305 and remove carbon nanostructures that havecollected on the collection surface. It is noted that the vessel 101,outlet conduit 135, tunnel upper wall 114, reactant liquid 105 andreactant liquid level 102 are identical to those shown in FIG. 1.

The alternative embodiment shown in FIG. 4, includes collectionstructures 401 similar to structure 301 shown in FIG. 3. However, theembodiment shown in FIG. 4 also includes additional blocking structures402 supported below the reactant liquid level 102. These blockingstructures 402 direct reaction products in the reactant liquid 105toward a central portion of each collection structure 401 so that thereaction products must flow around the collection structures to exit thereactant liquid. It will be noted that the view in FIG. 4 is at about 90degrees to the view in FIGS. 1 and 3. It will be further noted thatmultiple spaced apart flow channels at the outlet end 117 of a tunnelstructure such as that shown in FIG. 1 would be required to allow thereaction products to flow up properly beneath each of the blockingstructures 402 shown in FIG. 4.

The alternate collection arrangement shown in FIG. 5 includes a seriesof collection members 501 having vertically extending collectionsurfaces 502. The vertical orientation of surfaces 502 is in contrast tothe collection surface 110 shown in FIG. 1, which extends transverse tothe device vertical axis V. That is, the collection surfaces 502 extendparallel to device vertical axis V rather than transverse. Collectionmembers 501 may comprise cylinders or plates that are spaced apartsufficiently to allow effluent other than the materials to beincorporated in nanostructures to reach outlet conduit 135.

A method according to the present invention may now be described withreference particularly to the embodiment shown in FIG. 1. Such a methodincludes isolating carbon atoms from hydrocarbon molecules by reactionwithin or with a reactant liquid and maintaining the isolated carbonatoms in the reactant liquid for a sufficient period of time to placethe carbon atoms in the desired excited form as conditioned carbonanions. This step is performed in apparatus 100 in FIG. 1 by contactinga carbon-bearing feed material from supply 128 with the reactant liquidin vessel 101. Sufficient contact time to produce the conditioned carbonanions is achieved in apparatus 100 by ensuring that the feed materialand any intermediate reaction products must flow the entire length ofthe tunnel structure defined by upper tunnel wall 114 and side walls115. Also, the reactant liquid is maintained at a suitable reactiontemperature to effect the desired liberation of carbon atoms. Forexample, where the reactant liquid is made up predominantly of aluminumthe liquid is maintained between approximately 650 degrees Celsius andapproximately 950 degrees Celsius, and more preferably at approximately900 degrees Celsius. Injection point 104 and upper tunnel wall 114 arelocated deep enough in the reactant liquid to produce a desired reactionpressure, preferably at least 2.4 psig at least at some point in theapparatus where the reactant liquid comprises predominantly aluminum.These preferred temperatures and pressure conditions together with thenature of the reactant liquid ensure the production of the desiredconditioned carbon anions.

The time and energy required to liberate carbon atoms from thecarbon-bearing feed material will depend upon the nature of the feedmaterial. For example, assuming a feed material of CH₃, approximately1735.5 Btu of kinetic energy per mole of feed material will be requiredto liberate the carbon atoms from the CH₃ molecules. The energy requiredfor this carbon liberation step may also be calculated for othercarbon-bearing feed materials based on the bond energy required to breakthe chemical bonds to or between the carbon atoms in the respective feedmaterial. Additional energy is then required to produce the desiredconditioned carbon anions, that is, carbon anions at least at the SP3hybrid energy state. Specifically, about 11 eV of kinetic energy isrequired to energize the carbon from the ground state to the firstactivation energy level, and about another 1.88 eV of energy is requiredto move the carbon (that is, the electrons associated with the carbonatom) from the first activation energy to the second activation energylevel, which may be referred to as the 3PS2P2 energy state. From thispoint, additional energy in the amount of approximately 8 eV is requiredto move the electrons associated with the carbon atom from the secondactivation energy level to the 5S atomic structure of the SP3 hybridenergy state. Thus, once the chemical bonds of the feed stock are brokento isolate a carbon atom into the reactant liquid, the carbon thenrequires about 3.1703×10⁻²¹ Btus of energy per carbon atom, that is,about 25 electron volts of kinetic energy per atom, to be converted tothe desired conditioned carbon anions. It will be noted that theseconditioned carbon anions remain highly energetic while in the highenergy conditions of the liquid reactant, and remain highly energeticand unstable at the time they escape from the high energy conditions ofthe liquid reactant material, such as by eluding into the collectionchamber 107 shown in FIG. 1.

To produce carbon nanostructure from the conditioned carbon anionsgenerated in the reactant liquid, the conditioned carbon anions areallowed to traverse the surface of the reactant liquid in the effluentejection area 108, and are directed across collection surface 110 whichmay include one or more seed materials or objects. Collection conditionsare maintained in chamber 107 and at collection surface 110 at which theconditioned carbon anions phase change to a ground state by carbonnanostructure self-assembly.

Maintaining collection conditions in chamber 107 and at surface 110 mayinclude controlling the temperature and effluent flow conditions as wellas the appropriate atmosphere in chamber 107. In particular, anappropriate collection atmosphere comprises an atmosphere that does notchemically or physically interfere with the desired carbon nanostructureformation. Purging collection chamber 107 of materials that couldchemically react with the conditioned carbon anions before they can formthe desired nanocarbon structures may be particularly important increating and maintaining the desired collection atmosphere. Thus, apreferred process includes first purging the chamber 107 by directing asuitable purge gas such as argon or some other noble gas or an inert gasfrom purge supply 129 to chamber 107. A separate purge arrangement mayalternatively or additionally be included in the system with a purgeinlet directly in chamber 107 to prevent having to run the purge gasthrough the reactant liquid.

The flow regime of effluent exiting the reactant liquid and flowingthrough collection chamber 107 may be important for allowing theconditioned carbon anions to bond together to produce the desired carbonnanostructures without extraneous atoms becoming incorporated in thestructures. It is believed that a low velocity turbulent flow regimeover collection surface 110 (that is, a flow producing eddy currentsover the collection surface) best facilitates the production of carbonnanostructures without incorporating heavier atoms (such as metals) thatmay escape from the reactant liquid bath. It may also be possible toadjust the flow rate and composition of effluent flowing over collectionsurface in order to encourage the incorporation of various atoms otherthan carbon in the carbon nanostructures produced at the collectionsurface. The invention encompasses numerous techniques for controllingthe composition and flow rate of effluent through collection chamber 107and over collection surface 110. The relative amount of carbon-bearingfeed material in the material injected at point 104 and the type ortypes of hydrocarbon materials injected may influence both flow rate andcontent of flow. An inert or noble gas may be injected together with thefeed material from purge gas supply 129 or from some other supply toaffect the flow rate of effluent through chamber 107 and the content ofthe effluent.

Some forms of the invention may purposefully inject one or morematerials into the collection chamber 107 through a separate collectionchamber input, that is, separate from effluent ejection area 108, inorder to affect the flow characteristics in the flow chamber and inorder to provide desired materials to be incorporated in the carbonnanostructures. Such a separate collection chamber input may include asuitable tube (not shown) which traverses a collection chamber wall andwhich includes an injection end at a point to direct injected materialsagainst collection surface 110 and effluent flows up from the reactantliquid 105 and passes over the collection surface. Particles of seedmaterial may also be injected into collection chamber 107 with such aninjection conduit. These particles of seed material may be injectedprior to enabling the conditioned carbon anions to flow acrosscollection surface 110 or while conditioned carbon anions are flowingacross the collection surface.

Numerous other variations may be employed to produce the desired flowregime and flow characteristics through collection chamber 107. Twomethods are employed in apparatus 100 shown in FIG. 1. One methodemploys deflection surface 140 to deflect effluent escaping from thereactant liquid at effluent ejection area 108. This deflection ispreferably produced anywhere from just above the surface of the reactantliquid to approximately three feet above the surface of the reactantliquid. Other types of deflection surfaces or features may also beemployed according to the present invention. The other flow regime andcharacteristic affecting technique used the apparatus shown in FIG. 1comprises providing collection surface 110 in a transverse plane withrespect to device vertical axis V along which the effluent initiallyflows as it escapes the reactant liquid. Providing this transversecollection surface 110 produces a low pressure area on the collectionsurface in an area near the rightmost edge in FIG. 1. The low pressurearea created as effluent flows over the rightmost upper edge ofcollection structure 138 in FIG. 1 is believed to encourage thecollection of conditioned carbon anions at that location of collectionsurface 110 and the production of carbon nanostructures at thatlocation. It will be appreciated that numerous different collectionsurface profiles or contours may be employed to encourage the desiredcollection of conditioned carbon anions and self-assembly ofnanostructures. For example, collection surface 110 may include one ormore projections and/or indentations to produce the desired flowcharacteristics across the collection surface.

Any number of reactant liquids may be used to react the feed materialsor feed material constituents according to the present invention. Apreferred reactant liquid comprises liquid aluminum either alone or withother metals as disclosed in U.S. Pat. No. 5,000,101, which is alsoincorporated herein in its entirety. Temperatures may preferably rangefrom approximately 650 degrees Celsius to approximately 950 degreesCelsius for reactant metals incorporating a substantial fraction ofaluminum. Other reactant liquids may be used within differenttemperature ranges sufficient to liberate carbon atoms and place them inthe desired chemically excited state as conditioned carbon anions forassembly into nanostructures at collection surface 110. The inventionencompasses any liquid that either reacts with the feed material orotherwise causes carbon atoms to be liberated from the feed material andexcited to conditioned carbon anions. The carbon atoms may be liberatedby chemical reduction (as in the case of a reactant liquid made uppredominantly of aluminum), by chemical oxidation, by providingchemically neutral electron reduction potentials, or by applyingsufficient kinetic energy (through heat) to break the carbon bonds toother atoms in the feed molecules, or by any of these mechanisms.Liberated carbon atoms may then be converted to the desired conditionedcarbon anions by any suitable process, preferably by heat appliedthrough the reactant liquid. The reactant liquid may be a metal, acid,base, salt, or any combination of these. The temperature of theparticular liquid will depend upon the particular reaction required toliberate carbon atoms from the feed material and the nature of thereactant liquid itself. For example, chemically neutral liquids thatliberate carbon atoms by heat alone may be held at very hightemperatures to produce the desired carbon liberation, and excitation toconditioned carbon anions. Temperatures on the order of approximately1500 degrees Celsius or more may be required for carbon liberation andexcitation by heat alone.

Collection surface 110 is also preferably maintained in a similartemperature range as the reactant liquid, and most preferably at atemperature just below the reactant liquid temperature, for example,approximately fifty (50) degrees Celsius or less below the liquidreactant temperature. Thus, the collection surface 110 and collectionchamber 107 in areas near the collection surface will be isothermic ornearly isothermic with respect to the reactant liquid. It is believedthat these reactant liquids, and temperatures, together with thereaction pressure and contact time with the reactant liquid not onlyliberate the carbon atoms from the hydrocarbon feed material but alsoplaces the liberated carbon in the excited state as conditioned carbonanions. The reactant liquid is also believed to surround the liberatedcarbon atoms while they are still in the reactant liquid to maintain thecarbon atoms in the chemically excited state as conditioned carbonanions and prevent them from phase changing to a ground state beforethey have a chance to self-assemble into the desired nanostructures atthe collection surface 110. The conditions are maintained at thecollection surface according to the present invention so that theseconditioned carbon anions phase change to a ground state as they bondcovalently with other carbon atoms at the collection surface to form thedesired carbon nanostructures.

It will be appreciated that some carbon that escapes the reactant liquidmay also be diatomic carbon and double or triple bonded carbon. As usedin this disclosure and the accompanying claims, “liberated carbon atoms”includes single atom carbon, diatomic carbon, and other two-carboncombinations such as two-carbon double bonded structures and two-carbontriple bonded structures. All of the liberated carbon atoms as well asall surviving carbon molecules escaping the reactant liquid will also bechemically excited, that is, will have active electrons. Some of thetwo-carbon combinations and/or other surviving carbon molecules that mayescape the reactant liquid may be incorporated, together with single,chemically excited carbon atoms, into molecularly combined carbonnanostructures within the scope of the present invention.

The present invention may use any number of carbon-bearing compounds asthe feed material or as part of the feed material. Preferred forms ofthe invention utilize hydrocarbon compounds including single-bondedcarbon either predominantly or exclusively. However, compounds includingdouble and triple bonded carbon may be used according to the inventionprovided sufficient contact time with the reactant liquid to liberatecarbon atoms and energize them to conditioned carbon anions for assemblyinto carbon nanostructures, or to produce chemically excited carbonmolecules for assembly into carbon nanostructures. Some forms of theinvention may adjust the content of the various carbon-bearing materialsin a feed material mixture to provide a desired concentration ofliberated single carbon atoms and liberated carbon molecules forincorporation into the desired carbon nanostructures. For example, thefeed materials may be manipulated so that the effluent escaping thereactant liquid includes carbon in desired relative concentrations ofsingle carbon atoms and double bonded carbon molecules.

It is also noted that some reactant liquids are capable of liberatingcarbon atoms from highly stable forms of carbon. For example, thepreferred reactant liquid made up of aluminum or alloys of aluminum hasthe capability of liberating carbon atoms from even highly stable formsof carbon such as graphite and carbon nanostructures given sufficientcontact time. Thus, some types of reactant liquids, whether they operateby chemical reduction, chemical oxidation, pyrolysis, or by reactionsfrom acids, bases, or salts, may be used to destroy carbonnanostructures and recycle the carbon atoms from these materials indifferent types of carbon materials. In one aspect of the presentinvention, carbon nanostructure materials may be introduced into areactant liquid such as liquid aluminum or liquid aluminum alloy at 650to 950 degrees Celsius to isolate conditioned carbon anions from thecarbon nanostructure material. The conditioned carbon anions may then bedirected to a recovery area where the liberated carbon may be recovered.The recovery area may comprise a collection chamber such as chamber 107in FIG. 1 where the carbon anions may self-assemble into new carbonnanostructures. Alternatively, the recovery area may comprise acollection surface free area in which the carbon anions are encouragedto phase change to a ground state without self-assembly into carbonnanostructures.

Tests which were conducted according to the present invention may bedescribed with reference to the test apparatus 600 showndiagrammatically in FIG. 6. This test apparatus 600 included a vessel601 containing liquid reactant metal 602 made up of predominantlyaluminum together with a number of other metals at about 930 degreesCelsius. The liquid reactant metal 602 was continuously circulated toand from a heating chamber not shown in FIG. 6 with a stirring devicealso not shown in the figure. An injection/collection structure includedin test apparatus 600 was made up of an injection conduit 604 thatextended down from a top wall 605 to an injection point 606 below thelevel 607 of reactant metal 602. Subsurface deflecting elements 608helped prevent reaction products 609 from escaping the bath too quickly.A collection structure 610 included a rectangular plate generallycentered in vessel 601. Effluent escaping from the reactant metal 602traversed the surface of the metal at level 607 in areas A and in smallgaps G between injection conduit 604 and collection structure/plate 610.During the collection part of the test, plate 610 was mostly submergedin liquid metal 602 leaving at most about one-half inch of the platethickness above level 607.

In the tests, once the injection conduit/collection structure was inplace in vessel 601, argon gas was injected through input line 612 andultimately through conduit 604 and the reactant metal to displace airand any other gasses trapped in the area between level 607 and top 605which formed the collection area of the apparatus. Once the collectionarea was purged with argon gas, methane was injected through input 614at a rate of approximately four liters per minute for between thirty andforty-eight hours. Thereafter, acetylene gas and motor oil were alsopumped through conduit 604. The injection conduit/collection structurewas then removed from vessel 601 and allowed to cool in open air. Blacksoot-like material was observed over substantially the entire uppersurface of collection plate 610. This material was scraped off plate 610in several areas and observed through a scanning electron microscopedown to a resolution of approximately one micron and a transmissionelectron microscope at up to 200,000 times magnification. Theseobservations showed single-walled carbon nanotubes, double-walled carbonnanotubes, nanofibers, and carbon nanoropes in the sample material.

FIGS. 7 and 8 may be used to describe carbon nanostructures that may beproduced from the conditioned carbon anions generated beneath a surfaceof a reactant liquid according to the present invention. A novel qualityof carbon nanostructures produced from reactant liquid-generatedconditioned carbon anions is that substantially all other materials,including even hydrogen may be excluded from the resulting carbonnanostructures. The resulting carbon nanostructures are made up purelyof hexagonally arranged carbon atoms with each carbon atom having threecovalent bonds to adjoining carbon atoms and one unbound pi electron.FIG. 7 shows a small portion carbon nanostructure made up of a singlelayer of hexagonally arranged carbon atoms 701. This structure may beplanar or may be a portion of a nanotube wall. Each carbon atom 701includes three covalent bonds 702 to adjoining carbon atoms 701. Eachcarbon atom 701 also includes one unbound pi electron 703 having anorbital extending generally at a right angle to the plane of theadjacent hexagonal arrangement. The unbound pi electrons 703 are shownin the view of FIG. 7 as extending uniformly on one side of thehexagonal rings. However, it will be appreciated that carbonnanostructures according to the invention may be formed with unbound pielectrons arranged on each side of the hexagonal rings. That is, someunbound pi electrons may extend in the direction shown in FIG. 7, whileothers may extend in the opposite direction.

FIG. 8 shows a small portion of another carbon nanostructure made up ofhexagonal rings of carbon atoms 801. This structure, however, is made upof two distinct layers of hexagonally arranged carbon atoms, layer 802and layer 803. Each layer 802 and 803 may be planar or each may formpart of a tubular structure, a double-walled nanotube. As in thestructure of FIG. 7, each carbon atom 801 is covalently bonded to threeadjoining carbon atoms and includes an unbound pi electron 804 having anorbital extending generally perpendicular to the plane of the hexagonalstructure. Again, the unbound pi electrons need not all extend on oneside of the hexagonal structures, but may be interleaved or otherwiseextend on opposite sides of the hexagonal structures.

It is believed that the hydrogen-free and impurity-free carbonnanostructures illustrated in FIGS. 7 and 8 are produced by twocooperating factors according to the present invention. First, theconditioned carbon anions and other materials, such as hydrogen,released from a carbon-bearing feed material are maintained in anisolated state beneath the surface of the reactant liquid, eachcompletely surrounded by atoms of the reactant liquid, as individualseparate “islands” in the reactant liquid. Thus, there is no possibilityof contaminant incorporation with the carbon in the reactant liquiditself. Second, once the conditioned carbon anions and any energizedcarbon molecules escape from the bath to the isothermic or nearlyisothermic nanostructure collection surface (110 in FIG. 1), the energystates of all the non-carbon atoms remains such that the non-carbonatoms form antibonding molecular orbitals with respect to carbon. Thisformation of molecular orbitals in the non-carbon atoms prohibits thenon-carbon atoms, including hydrogen and any other atomic contaminants,from bonding with the eluding carbon anions and molecules. Rather, theeluding conditioned carbon anions rapidly phase change into carbonnanostructures while hydrogen atoms other non-carbon atoms eluding fromthe reactant liquid are carried on as effluent that eventually exits thesystem through outlet conduit 135 in the embodiment of FIG. 1.

The above described preferred embodiments are intended to illustrate theprinciples of the invention, but not to limit the scope of theinvention. Various other embodiments and modifications to thesepreferred embodiments may be made by those skilled in the art withoutdeparting from the scope of the present invention.

1. A method including: (a) introducing a carbon-bearing material into areactant liquid; (b) isolating carbon atoms from the carbon-bearingmaterial as conditioned carbide anions located below a surface of thereactant liquid; and (c) directing the conditioned carbide anions fromthe reactant liquid to a collection area.
 2. The method of claim 1wherein the reactant liquid is made up of one or more liquid metals. 3.The method of claim 2 wherein the reactant liquid includes predominantlyaluminum.
 4. The method of claim 3 wherein the reactant liquid is heldat a temperature of approximately 900 degrees Celsius.
 5. The method ofclaim 1 wherein the reactant liquid isolates carbon atoms from thecarbon-bearing material by chemical reduction, chemical oxidation, orpyrolysis, or by reactions from acids, bases, or salts.
 6. A method forplacing carbon atoms in a state to facilitate carbon nanostructureassembly, the method including: (a) isolating carbon atoms asconditioned carbide anions below a surface of a reactant liquid; and (b)enabling the conditioned carbide anions to escape from the reactantliquid to a collection area.
 7. The method of claim 6 wherein thereactant liquid is made up of one or more liquid metals.
 8. The methodof claim 7 wherein the reactant liquid includes predominantly aluminum.9. The method of claim 8 wherein the reactant liquid is held at atemperature of approximately 900 degrees Celsius.
 10. The method ofclaim 6 wherein the reactant liquid isolates carbon atoms from acarbon-bearing material by chemical reduction, chemical oxidation, orpyrolysis, or by reactions from acids, bases, or salts.
 11. A carbonstructure including at least one layer made up of hexagonally arrangedcarbon atoms, each carbon atom having three covalent bonds to adjoiningcarbon atoms and one unbound pi electron.
 12. The carbon structure ofclaim 11 wherein the layer of hexagonally arranged carbon atoms iswrapped around a central axis to form a tubular shape.
 13. The carbonstructure of claim 12 further including at least one additional layer ofhexagonally arranged carbon atoms, each carbon atom having one unboundpi electron and three covalent bonds to adjoining carbon atoms in therespective additional layer.
 14. A method including: (a) introducing amaterial made up of carbon nanostructures into a reactant liquid; (b)separating carbon atoms from the carbon nanostructures and isolating theseparated carbon atoms as conditioned carbide anions located below asurface of the reactant liquid; and (c) directing the conditionedcarbide anions from the reactant liquid to a recovery area.
 15. Themethod of claim 14 wherein the step of directing the conditioned carbideanions from the reactant liquid to the recovery area includes causingthe conditioned carbide anions to flow over a collection surface withinthe recovery area.
 16. The method of claim 14 wherein the step ofdirecting the conditioned carbide anions from the reactant liquid to therecovery area includes causing the conditioned carbide anions to flowalong a particle formation path through a phase changing area so thatthe liberated carbon atoms are enabled to phase change to the groundstate in the phase changing area.
 17. The method of claim 14 wherein thereactant liquid is made up of one or more liquid metals.
 18. The methodof claim 17 wherein the reactant liquid includes predominantly aluminum.19. The method of claim 18 wherein the reactant liquid is held at atemperature of approximately 900 degrees Celsius.
 20. The method ofclaim 14 wherein the reactant liquid isolates carbon atoms from thecarbon nanostructures by chemical reduction, chemical oxidation, orpyrolysis, or by reactions from acids, bases, or salts.